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Table 11 Estimated number of theoretical trays

From: Refinery Gas Treating Processes

Component

Mol/h

Ave K

VK/L

Stripout %

Mol/h

H2S

270

44

4.7

100

270

H2O

8,655

0.72

0.08

<0.5

8.0

HC

1.8

3.5

0.37

50

0.9

MEA

637.6

0.1

0.01

0

0

Total

8,564.3

   

278.9

Notes

  

Use 3 trays

From Fig. 6